Mixture of Tetrahydrofuran + Ethane, 1,1,2,2-tetrachloro-

Datasets

1. η - Viscosity, Pa*s
2. P_vap - Vapor or sublimation pressure, kPa
3. n₀ - Refractive index (Na D-line)
4. ρ_l - Mass density, kg/m3
5. c_sound,fluid - Speed of Sound, m/s
6. T_boil - Boiling temperature at pressure P, K

Viscosity, Pa*s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (1) - Liquid	Viscosity, Pa*s - Liquid
0.1023	0.0014
0.2128	0.0013
0.3093	0.0012
0.4056	0.0011
0.5093	0.0010
0.6032	0.0009
0.7046	0.0008
0.8008	0.0007
0.8973	0.0006

Vapor or sublimation pressure, kPa [ref]

Fixed		Measured
Temperature, K - Liquid	Mole fraction of Ethane, 1,1,2,2-tetrachloro- (2) - Liquid	Vapor or sublimation pressure, kPa - Liquid
283.15	0.0536	10.07
283.15	0.1168	9.18
283.15	0.2101	7.54
283.15	0.2724	6.44
283.15	0.3585	4.87
283.15	0.4236	3.85
283.15	0.5227	2.55
283.15	0.6101	1.69
283.15	0.6565	1.37
283.15	0.7444	0.92
283.15	0.7906	0.72
283.15	0.8433	0.55
283.15	0.9548	0.32
288.15	0.0537	12.84
288.15	0.1168	11.67
288.15	0.2102	9.66
288.15	0.2725	8.27
288.15	0.3586	6.30
288.15	0.4237	5.01
288.15	0.5228	3.36
288.15	0.6101	2.29
288.15	0.6566	1.88
288.15	0.7445	1.26
288.15	0.7906	0.99
288.15	0.8433	0.80
288.15	0.9548	0.47
293.15	0.0536	16.22
293.15	0.1169	14.76
293.15	0.2104	12.26
293.15	0.2727	10.49
293.15	0.3588	8.07
293.15	0.4238	6.48
293.15	0.5228	4.38
293.15	0.6102	3.01
293.15	0.6566	2.48
293.15	0.7445	1.69
293.15	0.7907	1.35
293.15	0.8433	1.08
293.15	0.9548	0.67
298.15	0.0537	20.30
298.15	0.1168	18.47
298.15	0.2106	15.38
298.15	0.2730	13.21
298.15	0.3590	10.24
298.15	0.4239	8.23
298.15	0.5229	5.64
298.15	0.6103	3.93
298.15	0.6567	3.24
298.15	0.7445	2.25
298.15	0.7907	1.80
298.15	0.8434	1.44
298.15	0.9548	0.89
303.15	0.0537	25.23
303.15	0.1169	22.97
303.15	0.2103	19.22
303.15	0.2727	16.55
303.15	0.3593	12.91
303.15	0.4241	10.44
303.15	0.5230	7.23
303.15	0.6104	5.09
303.15	0.6568	4.22
303.15	0.7446	2.97
303.15	0.7907	2.38
303.15	0.8434	1.92
303.15	0.9548	1.20
308.15	0.0537	30.96
308.15	0.1169	28.32
308.15	0.2105	23.72
308.15	0.2730	20.49
308.15	0.3596	16.02
308.15	0.4244	13.08
308.15	0.5232	9.15
308.15	0.6105	6.50
308.15	0.6569	5.42
308.15	0.7447	3.83
308.15	0.7908	3.13
308.15	0.8434	2.55
308.15	0.9548	1.58
313.15	0.0537	37.78
313.15	0.1170	34.58
313.15	0.2106	29.03
313.15	0.2731	25.14
313.15	0.3591	19.86
313.15	0.4240	16.26
313.15	0.5234	11.44
313.15	0.6107	8.18
313.15	0.6570	6.87
313.15	0.7448	4.90
313.15	0.7908	4.00
313.15	0.8434	3.28
313.15	0.9548	2.07
318.15	0.0538	45.78
318.15	0.1171	41.89
318.15	0.2109	35.24
318.15	0.2735	30.59
318.15	0.3592	24.31
318.15	0.4242	19.99
318.15	0.5238	14.20
318.15	0.6110	10.23
318.15	0.6572	8.64
318.15	0.7449	6.20
318.15	0.7909	5.14
318.15	0.8435	4.20
318.15	0.9548	2.69
323.15	0.0540	55.02
323.15	0.1173	50.43
323.15	0.2109	42.50
323.15	0.2738	36.95
323.15	0.3596	29.50
323.15	0.4244	24.40
323.15	0.5234	17.57
323.15	0.6114	12.73
323.15	0.6575	10.79
323.15	0.7452	7.79
323.15	0.7910	6.51
323.15	0.8436	5.37
323.15	0.9549	3.45

Refractive index (Na D-line) [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (1) - Liquid	Refractive index (Na D-line) - Liquid
0.1023	1.483
0.2128	1.476
0.3093	1.4701
0.4056	1.4639
0.5093	1.4556
0.6032	1.4472
0.7046	1.4368
0.8008	1.4268
0.8973	1.416

Mass density, kg/m3 [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (1) - Liquid	Mass density, kg/m3 - Liquid
0.1023	1523.21
0.2128	1460.02
0.3093	1401.59
0.4056	1340.18
0.5093	1270.31
0.6032	1203.28
0.7046	1126.91
0.8008	1050.12
0.8973	968.58

Speed of sound, m/s [ref]

Operational conditions:

• Temperature, K = 303.15 (Liquid)
• Pressure, kPa = 101.3 (Liquid)

Mole fraction of Tetrahydrofuran (1) - Liquid	Speed of sound, m/s - Liquid
0.1023	1138.0
0.2128	1143.0
0.3093	1149.0
0.4056	1157.0
0.5093	1168.0
0.6032	1180.0
0.7046	1195.0
0.8008	1212.0
0.8973	1231.0

Boiling temperature at pressure P, K [ref]

Operational condition: Pressure, kPa = 95.8 (Liquid)

Mole fraction of Tetrahydrofuran (1) - Liquid	Boiling temperature at pressure P, K - Liquid
0.0000	417.45
0.1565	406.55
0.3576	390.45
0.4812	379.65
0.6024	368.75
0.6944	360.35
0.8197	349.55
0.9009	342.15
1.0000	337.55

Sources

• Isothermal (vapour + liquid) equilibrium for binary mixtures of (tetrahydrofuran + 1,1,2,2-tetrachloroethane or tetrachloroethene) at nine temperatures
• Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
• Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa

Note: These property values are available through the Cheméo API. A free account gives you an access key.